CN105399269A - Dual-aeration gained microbiological treatment method for industrial wastewater - Google Patents
Dual-aeration gained microbiological treatment method for industrial wastewater Download PDFInfo
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- CN105399269A CN105399269A CN201510710392.5A CN201510710392A CN105399269A CN 105399269 A CN105399269 A CN 105399269A CN 201510710392 A CN201510710392 A CN 201510710392A CN 105399269 A CN105399269 A CN 105399269A
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Abstract
The invention relates to the technical field of environmental engineering, and particularly relates to a dual-aeration gained microbiological treatment method for industrial wastewater. The method comprises the following steps: 1) filtering wastewater; 2) carrying out air flotation treatment on the wastewater so as to remove oily impurities; 3) carrying out secondary filtering on the wastewater; 4) carrying out pH value adjustment on the wastewater; 5) carrying out heavy metal ion sedimentation on the wastewater; 6) neutralizing the wastewater; 7) carrying out first aeration on the wastewater; 8) carrying out ion exchange on the wastewater by using cation exchange resin; 9) carrying out biodegradation on the wastewater; and 10) carrying out second aeration on the wastewater, so that reusable water is obtained. The dual-aeration gained microbiological treatment method for industrial wastewater provided by the invention is stable in running, and high in production efficiency; through a dual-aeration process, a microbiological treatment step is significantly gained, so that the cost and time of the microbiological treatment step are effectively reduced, the efficiency of the whole process is improved, and the quality of effluent water is good and stable.
Description
Technical field
The present invention relates to field of environment engineering technology, be specifically related to a kind of two aeration gain microbial treatment methods of trade effluent.
Background technology
Trade effluent, after primary treatment, still has a lot of impurity to be difficult to process, such as: organic chloride, comprises the chlorine-containing organic compounds such as chlorinated aliphatic hydrocarbon, chlorination aromatic hydrocarbon in sewage.The chemical property of organic chloride is relatively stable, easily accumulates in the organic matter of organism, soils and sediments, and in occurring in nature degraded slowly, the environmental hazard cycle is long.
At present, the treatment process of the comparatively ripe all kinds of stain disease of biochemical treatment grown up gradually has been had.But, along with country is to the raising of environmental requirement, also more and more higher to the requirement of sewage disposal and sewage discharge, if the more efficient biochemical treatment process by sewage disposal more organically combines, be the problem along with the development need of water treatment field solves further.
Summary of the invention
For solving the deficiencies in the prior art, the invention provides a kind of two aeration gain microbial treatment methods of trade effluent.
Two aeration gain microbial treatment methods for trade effluent, comprise the steps:
1) waste water is filtered, remove macrobead solid sundries and suspending sundries;
2) air-flotation process is carried out to waste water, removing oiliness impurity;
3) secondary filtration is carried out to waste water, remove suspending sundries;
4) pH value adjustment is carried out to waste water;
5) heavy metal ion precipitation is carried out to waste water;
6) waste water is neutralized;
7) first time aeration is carried out to waste water;
8) by Zeo-karb, ion-exchange is carried out to waste water;
9) biological degradation is carried out to waste water;
10) carry out second time aeration to waste water, obtaining can reuse water.
Concrete, step 9) in add nutritious dose and composite fungus agent.
Concrete, described nutrition agent comprises starch, glucose, urea, Sodium phosphate dibasic, potassium primary phosphate and magnesium sulfate.
Concrete, described composite fungus agent comprises proteolytic enzyme, amylase, cellulase, lipase, nitrobacteria, lactobacillus and yeast flora.
Preferably, step 4) in pH value be adjusted to 7.0 ~ 8.5.
Two aeration gain microbial treatment methods of trade effluent provided by the present invention are stable, production efficiency is high, by two aeration system, significant gain has been carried out to microbiological treatment step, effectively reduce cost and the time of microbiological treatment step, improve the efficiency of integrated artistic, water outlet quality better and water outlet stay in grade.
Embodiment
Be described principle of the present invention and feature below, illustrated embodiment, only for explaining the present invention, is not intended to limit scope of the present invention.
Embodiment 1
Two aeration gain microbial treatment methods for trade effluent, comprise the steps:
1) waste water is filtered, remove macrobead solid sundries and suspending sundries;
2) air-flotation process is carried out to waste water, removing oiliness impurity;
3) secondary filtration is carried out to waste water, remove suspending sundries;
4) carry out pH value adjustment to waste water, pH value is adjusted to 8.5;
5) heavy metal ion precipitation is carried out to waste water;
6) waste water is neutralized;
7) first time aeration is carried out to waste water;
8) by Zeo-karb, ion-exchange is carried out to waste water;
9) biological degradation is carried out to waste water;
10) carry out second time aeration to waste water, obtaining can reuse water.
Wherein, step 9) in add nutritious dose and composite fungus agent.Nutrition agent comprises starch, glucose, urea, Sodium phosphate dibasic, potassium primary phosphate and magnesium sulfate.Composite fungus agent comprises proteolytic enzyme, amylase, cellulase, lipase, nitrobacteria, lactobacillus and yeast flora.
Embodiment 2
Two aeration gain microbial treatment methods for trade effluent, comprise the steps:
1) waste water is filtered, remove macrobead solid sundries and suspending sundries;
2) air-flotation process is carried out to waste water, removing oiliness impurity;
3) secondary filtration is carried out to waste water, remove suspending sundries;
4) carry out pH value adjustment to waste water, pH value is adjusted to 7.5;
5) heavy metal ion precipitation is carried out to waste water;
6) waste water is neutralized;
7) first time aeration is carried out to waste water;
8) by Zeo-karb, ion-exchange is carried out to waste water;
9) biological degradation is carried out to waste water;
10) carry out second time aeration to waste water, obtaining can reuse water.
Wherein, step 9) in add nutritious dose and composite fungus agent.Nutrition agent comprises starch, glucose, urea, Sodium phosphate dibasic, potassium primary phosphate and magnesium sulfate.Composite fungus agent comprises proteolytic enzyme, amylase, cellulase, lipase, nitrobacteria, lactobacillus and yeast flora.
Embodiment 3
Two aeration gain microbial treatment methods for trade effluent, comprise the steps:
1) waste water is filtered, remove macrobead solid sundries and suspending sundries;
2) air-flotation process is carried out to waste water, removing oiliness impurity;
3) secondary filtration is carried out to waste water, remove suspending sundries;
4) carry out pH value adjustment to waste water, pH value is adjusted to 8.0;
5) heavy metal ion precipitation is carried out to waste water;
6) waste water is neutralized;
7) first time aeration is carried out to waste water;
8) by Zeo-karb, ion-exchange is carried out to waste water;
9) biological degradation is carried out to waste water;
10) carry out second time aeration to waste water, obtaining can reuse water.
Wherein, step 9) in add nutritious dose and composite fungus agent.Nutrition agent comprises starch, glucose, urea, Sodium phosphate dibasic, potassium primary phosphate and magnesium sulfate.Composite fungus agent comprises proteolytic enzyme, amylase, cellulase, lipase, nitrobacteria, lactobacillus and yeast flora.
Effect example
Adopt the method for embodiment 1, embodiment 2 and embodiment 3 respectively to 8t waste water, process, after process in 5 hours, effluent quality index all reaches index shown in following table, and sewage disposal actual processing effect is good.
Unit: mg/L
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, within the spirit and principles in the present invention all, any amendment done, equivalent replacement, improvement etc., all should be included within protection scope of the present invention.
Claims (5)
1. two aeration gain microbial treatment methods for trade effluent, is characterized in that, comprise the steps:
1) waste water is filtered, remove macrobead solid sundries and suspending sundries;
2) air-flotation process is carried out to waste water, removing oiliness impurity;
3) secondary filtration is carried out to waste water, remove suspending sundries;
4) pH value adjustment is carried out to waste water;
5) heavy metal ion precipitation is carried out to waste water;
6) waste water is neutralized;
7) first time aeration is carried out to waste water;
8) by Zeo-karb, ion-exchange is carried out to waste water;
9) biological degradation is carried out to waste water;
10) carry out second time aeration to waste water, obtaining can reuse water.
2. two aeration gain microbial treatment methods of trade effluent according to claim 1, is characterized in that: step 9) in add nutritious dose and composite fungus agent.
3. two aeration gain microbial treatment methods of trade effluent according to claim 2, is characterized in that: described nutrition agent comprises starch, glucose, urea, Sodium phosphate dibasic, potassium primary phosphate and magnesium sulfate.
4. two aeration gain microbial treatment methods of trade effluent according to claim 3, is characterized in that: described composite fungus agent comprises proteolytic enzyme, amylase, cellulase, lipase, nitrobacteria, lactobacillus and yeast flora.
5., according to two aeration gain microbial treatment methods of the arbitrary described trade effluent of Claims 1-4, it is characterized in that: step 4) middle pH value is adjusted to 7.0 ~ 8.5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201510710392.5A CN105399269A (en) | 2015-10-27 | 2015-10-27 | Dual-aeration gained microbiological treatment method for industrial wastewater |
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| CN201510710392.5A CN105399269A (en) | 2015-10-27 | 2015-10-27 | Dual-aeration gained microbiological treatment method for industrial wastewater |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109650600A (en) * | 2019-01-31 | 2019-04-19 | 珠海纳米德水处理科技有限公司 | A kind of industrial wastewater treatment system |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN85102690A (en) * | 1985-04-02 | 1986-10-01 | 华东化工学院 | A kind of method of administering cyanide wastewater |
| CN86108101A (en) * | 1986-12-30 | 1988-08-24 | 曾祥仁 | The integrated conduct method that contains heavy metal containing sewage |
| CN1605572A (en) * | 2003-10-08 | 2005-04-13 | 上海创博生态工程有限公司 | Microbiological ammonia nitrogen aligning agent and method for making the same |
| CN101037243A (en) * | 2007-04-26 | 2007-09-19 | 陈启松 | Heavy metal treatment method of electroplating wastewater |
| CN101070206A (en) * | 2006-05-12 | 2007-11-14 | 汉达精密电子(昆山)有限公司 | Chemical copper-plating rinsing waste-water treatment process |
| CN101676225A (en) * | 2008-09-16 | 2010-03-24 | 佛山市楚一科技有限公司 | A new microbe agent and preparation method thereof |
| KR101393712B1 (en) * | 2014-01-23 | 2014-05-13 | 이길환 | Treatment method of livestock waste water and device thereof |
| CN203768167U (en) * | 2014-03-14 | 2014-08-13 | 杨昕 | Wastewater treatment device for environmental engineering |
| CN204151203U (en) * | 2014-09-29 | 2015-02-11 | 广西壮族自治区环境保护科学研究院 | A kind of dangerous waste disposal center Waste Water Treatment |
| CN104671588A (en) * | 2015-01-06 | 2015-06-03 | 江苏理文造纸有限公司 | Method for treating pulping and papermaking wastewater |
-
2015
- 2015-10-27 CN CN201510710392.5A patent/CN105399269A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN85102690A (en) * | 1985-04-02 | 1986-10-01 | 华东化工学院 | A kind of method of administering cyanide wastewater |
| CN86108101A (en) * | 1986-12-30 | 1988-08-24 | 曾祥仁 | The integrated conduct method that contains heavy metal containing sewage |
| CN1605572A (en) * | 2003-10-08 | 2005-04-13 | 上海创博生态工程有限公司 | Microbiological ammonia nitrogen aligning agent and method for making the same |
| CN101070206A (en) * | 2006-05-12 | 2007-11-14 | 汉达精密电子(昆山)有限公司 | Chemical copper-plating rinsing waste-water treatment process |
| CN101037243A (en) * | 2007-04-26 | 2007-09-19 | 陈启松 | Heavy metal treatment method of electroplating wastewater |
| CN101676225A (en) * | 2008-09-16 | 2010-03-24 | 佛山市楚一科技有限公司 | A new microbe agent and preparation method thereof |
| KR101393712B1 (en) * | 2014-01-23 | 2014-05-13 | 이길환 | Treatment method of livestock waste water and device thereof |
| CN203768167U (en) * | 2014-03-14 | 2014-08-13 | 杨昕 | Wastewater treatment device for environmental engineering |
| CN204151203U (en) * | 2014-09-29 | 2015-02-11 | 广西壮族自治区环境保护科学研究院 | A kind of dangerous waste disposal center Waste Water Treatment |
| CN104671588A (en) * | 2015-01-06 | 2015-06-03 | 江苏理文造纸有限公司 | Method for treating pulping and papermaking wastewater |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109650600A (en) * | 2019-01-31 | 2019-04-19 | 珠海纳米德水处理科技有限公司 | A kind of industrial wastewater treatment system |
| CN109650600B (en) * | 2019-01-31 | 2024-01-26 | 珠海纳米德水处理科技有限公司 | Industrial wastewater treatment system |
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